Gas phase aluminium extracting and silicon supplementing method of molecular sieve

A technology of extracting aluminum to supplement silicon and molecular sieves, which is applied in the fields of crystalline aluminosilicate zeolite, tobacco, and other applications, can solve the problems of difficult control of reaction conditions, uneven reaction temperature, poor heat transfer performance, etc., and achieve easy large-scale industrial application, ease of control, and the effect of reducing losses and emissions

Active Publication Date: 2006-11-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] Since the method provided by the invention is carried out under stirring, the molecular sieve solid particles are evenly rolled under stirring, which not only overcomes the poor mass transfer and heat transfer performance of the fixed bed, the difficult control of the reaction conditions, and the uneven reaction temperature, which is easy to cause local overheating It also makes the contact reaction between silicon tetrachloride gas and molecular sieve solid particles more uniform, easy to control, and avoids the phenomenon of coalescence of molecular sieve solid particles into dense lumps. Therefore, molecular sieves with more uniform properties can be obtained product

Method used

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  • Gas phase aluminium extracting and silicon supplementing method of molecular sieve
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  • Gas phase aluminium extracting and silicon supplementing method of molecular sieve

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Embodiment approach 1

[0029] The first specific embodiment of the present invention is as follows figure 1shown. Described reaction equipment comprises a reactor 1, a feed port 2 and a gas outlet 3, also has a stirrer 4 inside the reactor 1, and wherein, a gas-solid separator 5 is installed on the gas outlet 3, gas The hole diameter and porosity of the holes contained in the solid separator 5 ensure that the gas can pass through but the solid particles cannot pass through. The stirring rod of the stirrer 4 stretches out of the reaction kettle 1, and the place where the stirring rod contacts the reaction kettle 1 is airtight, so that the reaction kettle 1 is not connected to the outside world.

[0030] When carrying out aluminum extraction and silicon supplementation, molecular sieve solid particles are loaded from the feed port 2, the agitator 4 is started, and silicon tetrachloride liquid is added, and the feed port 2 and the gas outlet 3 are sealed. Heat the reaction kettle 1 to the reaction t...

Embodiment approach 2

[0032] The second specific embodiment of the present invention is as figure 2 shown. The reaction device includes all components of the first embodiment, and also includes an air inlet 6 . The air inlet 6 can be located at any position of the reactor 1 , preferably, the feed inlet 2 and the gas outlet 3 are located at the upper part of the reactor 1 , and the air inlet 6 is located at the lower part of the reactor 1 . Air inlet 6 is used to add silicon tetrachloride liquid. With the air inlet 6, the silicon tetrachloride liquid is added from the air inlet 6, and the feed inlet 2 is specially used for adding molecular sieve solid particles, and the operation is more convenient.

[0033] When performing aluminum extraction and silicon supplementation, molecular sieve solid particles are loaded from the feed port 2, the agitator 4 is started, and the feed port 2 and the gas outlet 3 are sealed. Add silicon tetrachloride liquid from air inlet 6, air inlet 6 is airtight or the ...

Embodiment approach 3

[0035] The third specific embodiment of the present invention is as image 3 shown. The reaction equipment includes all the components of the second specific embodiment, and a gas distributor 9 is installed on the top of the air inlet 6, and the top of the gas distributor 9 is on a plane or at the height of the bottom of the reactor 1. On the plane where the bottom of the reactor 1 is located. The function of the gas distributor is to enable the silicon tetrachloride gas to enter the reactor 1 continuously and evenly, and at the same time, ensure that the molecular sieve solid particles do not enter the pipeline connected to the air inlet 6 .

[0036] When carrying out aluminum extraction and silicon supplementation, molecular sieve solid particles are loaded from the feed port 2, the feed port 2 and the gas outlet 3 are sealed, the agitator 4 is started, and the feed port 2 is sealed. Add silicon tetrachloride liquid from air inlet 6, air inlet 6 is sealed or the pressure t...

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Abstract

The gas phase method of extracting aluminum from and supplementing silicon to molecular sieve is to contact molecular sieve with silicon tetrachloride inside one reaction apparatus. The reaction apparatus includes one reactor with material inlet, gas outlet and stirrer, and one gas-solid separator in the gas outlet. The gas-solid separator has suck pore diameter and porosity that the gas can pass through and the solid particle can not. The stirrer has stirring rod extending beyond the reactor hermetically. The contact under stirring has contact temperature of 100-500 deg.c and time of 5-10 min, and the weight ratio between the molecular sieve and silicon tetrachloride is 1 to 0.05-0.5. The said method homogeneous contact reaction between gaseous silicon tetrachloride and solid molecular sieve, no coagulation of solid molecular sieve, less environmental pollution, lowered production cost and other advantages, and is suitable for industrial production.

Description

technical field [0001] The invention relates to a method for extracting aluminum and supplementing silicon from a molecular sieve, more specifically to a method for extracting aluminum and supplementing silicon in a gas phase of a molecular sieve. Background technique [0002] Molecular sieves are widely used materials, such as active components of catalysts and adsorbents. According to different needs, various modifications can be made to molecular sieves. For example, in the field of catalysis, there is a greater demand for high-silicon molecular sieves. [0003] In the prior art, there are roughly three methods for extracting aluminum from molecular sieves to increase the silicon content of molecular sieves, namely, chemical aluminum extraction, hydrothermal aluminum extraction, and gas phase aluminum extraction for silicon supplementation. [0004] The method of chemically extracting aluminum is generally to use an acidic solution to conta...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B39/06A24F47/00
CPCA24F47/008C01B39/06
Inventor 杜军李峥周灵萍朱玉霞田辉平
Owner CHINA PETROLEUM & CHEM CORP
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